CN106366152A - Method of extracting asiaticoside from centella asiatica - Google Patents

Method of extracting asiaticoside from centella asiatica Download PDF

Info

Publication number
CN106366152A
CN106366152A CN201610726900.3A CN201610726900A CN106366152A CN 106366152 A CN106366152 A CN 106366152A CN 201610726900 A CN201610726900 A CN 201610726900A CN 106366152 A CN106366152 A CN 106366152A
Authority
CN
China
Prior art keywords
asiaticoside
herba centellae
extract
ethanol
mixed liquor
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201610726900.3A
Other languages
Chinese (zh)
Other versions
CN106366152B (en
Inventor
黄健军
谢冬养
陆美珍
叶出良
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanning Chengtai Biotechnology Co ltd
Original Assignee
Guilin Yi Tiancheng Biotechnology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Guilin Yi Tiancheng Biotechnology Co Ltd filed Critical Guilin Yi Tiancheng Biotechnology Co Ltd
Priority to CN201610726900.3A priority Critical patent/CN106366152B/en
Publication of CN106366152A publication Critical patent/CN106366152A/en
Application granted granted Critical
Publication of CN106366152B publication Critical patent/CN106366152B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07JSTEROIDS
    • C07J63/00Steroids in which the cyclopenta(a)hydrophenanthrene skeleton has been modified by expansion of only one ring by one or two atoms
    • C07J63/008Expansion of ring D by one atom, e.g. D homo steroids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Steroid Compounds (AREA)

Abstract

The invention discloses a method of extracting asiaticoside from centella asiatica. The method includes the steps of: 1) crushing the centella asiatica, and performing reflux extraction with a 60-70% ethanol solution, filtering an extract liquid to obtain a filtrate, recycling the solvent from the filtrate, adding water at 40-50 DEG C to dissolve the extract liquid to obtain a crude extract liquid; 2) adding rare earth salt to the crude extract liquid, and uniformly mixing and stirring the mixed liquid; 3) enabling the mixed liquid to pass through a X-5 macroporous resin column, wherein the mixed liquid is washed to colorless by water and then is eluted by ethanol being 50-70% in volume concentration, and collecting an eluant, recycling the ethanol and drying the eluant to obtain the asiaticoside. The method is high in purity and yield of the asiaticoside.

Description

The method extracting asiaticoside from Herba Centellae
Technical field
The invention belongs to technical field of biological extraction and in particular to a kind of from Herba Centellae extract asiaticoside method.
Background technology
Herba Centellae (centella asiatica (l.) urban) is Umbelliferae Herba Centellae tree plant, because its leaf exactly likes horse Shoes or half copper coin, so also known as Herba Calthae Membranaceae, Herba Glechomae etc., among the people also have place to be called pennyroyal mint, marchantia grass etc..Accumulated snow Applicating history in the traditional medicine field of many countries and regions for the grass is long, China's Chinese medicine to for oral administration of Herba Centellae and The existing bimillennium history of external, is recorded by Shennong's Herbal one book earliest.Record according to Compendium of Material Medica, Herba Centellae bitter in the mouth, Pungent, cold in nature, nontoxic, return liver,spleen,kidney, stomach, its effect is promoting blood circulation, reducing swelling and alleviating pain, and has heat-clearing and toxic substances removing, diuresis etc..Herba Centellae Chemical composition mainly have triterpeness, flavonoid, polyacetylene alkenes and volatile oil etc..Triterpeness mainly have triterpene saponin, such as Asiaticoside, asiaticoside etc., and triterpene acids, such as asiatic acid, Madecassic acid etc..The chemical composition of Herba Centellae In, Triterpene saponins are that research is earliest, a biological activity research big class component the most deep.Asiatic centella total saponins are mainly by amassing Asiaticoside and asiaticoside composition, they belong to the pentacyclic triterpene saponin of Ursane, be Herba Centellae pharmacologically active Main component.Asiaticoside typically first uses extract by solvents, then carries out purification using the less macroporous resin of average pore size, such as Hpd-100 (average pore size is 8.5~9.0nm), hpd-300 (average pore size is 5.0~5.5nm), because macroporous resin is to mesh The absorption of mark composition and screening specific aim are not very strong, and in adsorption process, a lot of impurity can be adsorbed onto in resin voids, and solves During suction, because hole is less, target component can not desorbing completely, therefore, the yield of asiaticoside after purification and purity are equal Not high.
Content of the invention
Present invention solves the technical problem that being to provide a kind of method extracting asiaticoside from Herba Centellae, the method is extracted The asiaticoside yield obtaining is big, and purity is high.
The technical scheme that the present invention provides is to provide a kind of method extracting asiaticoside from Herba Centellae, walks including following Rapid:
1) Herba Centellae is pulverized, with 60~70v% ethanol solution reflux, extract, extracting solution is filtered, filtrate recycling design, Plus 40 again~50 DEG C of water dissolutioies, obtain crude extract;
2) add rare-earth salts mixing toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, first it is washed to colourless, then use volumetric concentration to be 35~45v% Ethanol elution, thin layer chromatography tracing detection, collect the ethanol elution containing target component, reclaim ethanol, be dried, obtain Herba Centellae Glycosides.
Step 1) in, the consumption of ethanol is 10~20 times of Herba Centellae weight, reflux, extract, 1~3 time, 1~3h every time.
Volumetric concentration is 60~70% ethanol triterpene substance that can fully dissolve in Herba Centellae, including the total soap of triterpeness Glycosides and triterpene acid.Asiatic centella total saponins are many due to being often combined with most glycan molecules, hydroxy number in their molecule, Certain hydrophilic can be shown, but hydrophilic is not strong, be slightly soluble in water, and triterpene acids polarity less it is impossible to be dissolved in water In.Therefore asiaticoside can be helped to dissolve using 40~50 DEG C of warm water, Herba Centellae acid is insoluble in water, to reach Purpose except Triterpene acids.
Step 2) in, described rare-earth salts is rare earth chloride, rare earth sulfate or rare earth nitrate.Rare earth chloride is permissible It is lanthanum chloride, cerium chloride, praseodymium chloride, Neodymium chloride, samarium trichloride, Europium chloride, Gadolinium trichloride, terbium chloride, Dysprosium trichloride, Holmium trichloride, chlorination Erbium, thulium chloride, Ytterbium trichloride, lutecium chloride, Scium chloride (Sc4Cl12) and Yttrium chloride(Y2Cl6);Rare earth sulfate can be lanthanum sulfate, cerous sulfate, Dipraseodymium trisulfate, Dineodymium trisulfate, samarium sulphate, europium sulfate, Digadolinium trisulfate, sulphuric acid terbium, Dysprosium sesquisulfate, sulphuric acid holmium, erbium sulfate, thulium sulfate, Ytterbium Sulfate, sulphuric acid lutecium, Scium sulfate (Sc2(SO4)3) and Yttrium sesquisulfate;Rare earth nitrate can be Lanthanum (III) nitrate, cerous nitrate, praseodymium nitrate, neodymium nitrate, samaric nitrate, europium nitrate, nitric acid Gadolinium, Terbium nitrate (Tb(NO3)3), Dysprosium trinitrate, holmium nitrate, Erbium trinitrate, thulium nitrate, Ytterbium(III) nitrate., lutecium nitrate, Scium nitrate(Sc(NO3)3) and Yttrium trinitrate.
Oxygen atom on hydroxyl on rare earth element and asiaticoside and asiaticoside, carboxyl formed coordinate bond and, shape Become chemical affinity, according to hsab theory, because rare earth is hard acid, asiaticoside and asiaticoside are soft bases, because This, both combinations are not especially to consolidate.
Rare-earth salts accounts for the 0.1~0.5% of mixed liquor gross weight.Now, rare-earth salts can be fully coordinated with target component.
Step 3) in, x-5 model macroporous resin is non-polar resin, and particle diameter is 0.3~1.25mm, and specific surface area is 500 ~600m2/ g, average pore size is 29~30nm.Its aperture is far longer than the molecular particle size of asiaticoside.And the ligancy of rare earth Larger, with its carry out coordinate bond and oxygen-containing functional group number often do not reach its highest ligancy, therefore rare earth also can with big C in the resin of hole produces crosslinked, to reach the effect of absorption.
In order to ensure the crosslinking of rare earth element and macroporous resin, the upper prop speed of mixed liquor is less, and effect is better, through application People's many experiments, mixed liquor upper prop speed is 0.5~0.8bv/h, and cross-linking effect is best.
Due to rare earth element and asiaticoside and asiaticoside combination very built on the sand, and asiaticoside and ethanol Affinity extremely strong it is easy to be eluted by ethanol solution.There is hydroxyl due on three sites of asiaticoside, these three positions again Point is all that coordination atom is coordinated with rare earth atom, and asiaticoside hydroxyl more than asiaticoside, coordination ability Higher.Therefore, in eluting, asiaticoside is first eluted.The ethanol being 35~45% using volumetric concentration can preferentially by Asiaticoside eluting, and it is not mixed into asiaticoside.Elution speed is advisable for 2~2.5bv/h.
Compared with prior art, this method carries out adsorption and desorption, the asiaticoside yield of extraction for target component Up to more than 95%, high purity more than 99.5%.
Specific embodiment
The present invention is further elaborated for specific examples below, but not as a limitation of the invention.
Following percent is percentage by volume.
Embodiment 1
1) Herba Centellae is pulverized, 60% ethanol solution reflux, extract, of 10 times of Herba Centellae gross weight of addition 1 time, each 1h, will Extracting solution filter, by filtrate recycling design, then plus 40 DEG C of water dissolutioies, remove filtering residue, obtain final product crude extract;
2) add its weight 0.1% lanthanum chloride to mix toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, upper prop speed is 0.5bv/h, is first washed to colourless, then uses body Long-pending concentration is 35v% ethanol elution, and thin layer chromatography tracing detection collects the ethanol elution containing target component, reclaims ethanol, does Dry, obtain asiaticoside.
Through hlpc analysis, the response rate of asiaticoside is more than 95.24%, high purity more than 99.50%.
Embodiment 2
1) Herba Centellae is pulverized, 70% ethanol solution reflux, extract, of 20 times of Herba Centellae gross weight of addition 3 times, each 3h, will Extracting solution merge, filter, by filtrate recycling design, then plus 50 DEG C of water dissolutioies, remove filtering residue, obtain final product crude extract;
2) add its weight 0.5% cerous sulfate to mix toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, upper prop speed is 0.8bv/h, is first washed to colourless, then uses body Long-pending concentration is 45v% ethanol elution, and thin layer chromatography tracing detection collects the ethanol elution containing target component, reclaims ethanol, does Dry, obtain asiaticoside.
Through hlpc analysis, the response rate of asiaticoside is more than 95.33%, high purity more than 99.58%.
Embodiment 3
1) Herba Centellae is pulverized, 65% ethanol solution reflux, extract, of 15 times of Herba Centellae gross weight of addition 2 times, each 2h, will Extracting solution merge, filter, by filtrate recycling design, then plus 45 DEG C of water dissolutioies, remove filtering residue, obtain final product crude extract;
2) add its weight 0.2% praseodymium nitrate to mix toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, upper prop speed is 0.6bv/h, is first washed to colourless, then uses body Long-pending concentration is 40v% ethanol elution, and thin layer chromatography tracing detection collects the ethanol elution containing target component, reclaims ethanol, does Dry, obtain asiaticoside.
Through hlpc analysis, the response rate of asiaticoside is more than 95.18%, high purity more than 99.55%.
Embodiment 4
1) Herba Centellae is pulverized, 70% ethanol solution reflux, extract, of 10 times of Herba Centellae gross weight of addition 3 times, each 1h, will Extracting solution merge, filter, by filtrate recycling design, then plus 50 DEG C of water dissolutioies, remove filtering residue, obtain final product crude extract;
2) add its weight 0.1% Erbium trichloride to mix toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, upper prop speed is 0.5bv/h, is first washed to colourless, then uses body Long-pending concentration is 45v% ethanol elution, and thin layer chromatography tracing detection collects the ethanol elution containing target component, reclaims ethanol, does Dry, obtain asiaticoside.
Through hlpc analysis, the response rate of asiaticoside is more than 95.09%, high purity more than 99.63%.

Claims (6)

1. from Herba Centellae extract asiaticoside method it is characterised in that: comprise the following steps:
1) Herba Centellae is pulverized, with 60~70v% ethanol solution reflux, extract, extracting solution is filtered, filtrate recycling design, then plus 40~50 DEG C of water dissolutioies, obtain crude extract;
2) add rare-earth salts mixing toward crude extract, stir evenly, obtain mixed liquor;
3) by x-5 model macroporous resin column on mixed liquor, first it is washed to colourless, then use volumetric concentration to be 35~45v% ethanol Eluting, thin layer chromatography tracing detection, collect the ethanol elution containing target component, reclaim ethanol, be dried, obtain asiaticoside.
2. according to claim 1 from Herba Centellae extract asiaticoside method it is characterised in that: step 1) in, second The consumption of alcohol is 10~20 times of Herba Centellae weight, reflux, extract, 1~3 time, 1~3h every time.
3. according to claim 1 from Herba Centellae extract asiaticoside method it is characterised in that: step 2) in, institute Stating rare-earth salts is rare earth chloride, rare earth sulfate or rare earth nitrate.
4. according to claim 1 from Herba Centellae extract asiaticoside method it is characterised in that: step 2) in, dilute Earth salt accounts for the 0.1~0.5% of mixed liquor gross weight.
5. according to claim 1 from Herba Centellae extract asiaticoside method it is characterised in that: step 3) in, mix Conjunction liquid upper prop speed is 0.5~0.8bv/h.
6. according to claim 1 from Herba Centellae extract asiaticoside method it is characterised in that: step 3) in, wash De- speed is 2~2.5bv/h.
CN201610726900.3A 2016-08-25 2016-08-25 The method that asiaticosid is extracted from centella Active CN106366152B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610726900.3A CN106366152B (en) 2016-08-25 2016-08-25 The method that asiaticosid is extracted from centella

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610726900.3A CN106366152B (en) 2016-08-25 2016-08-25 The method that asiaticosid is extracted from centella

Publications (2)

Publication Number Publication Date
CN106366152A true CN106366152A (en) 2017-02-01
CN106366152B CN106366152B (en) 2018-01-19

Family

ID=57879131

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610726900.3A Active CN106366152B (en) 2016-08-25 2016-08-25 The method that asiaticosid is extracted from centella

Country Status (1)

Country Link
CN (1) CN106366152B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320580A (en) * 2018-10-30 2019-02-12 天峨县科学技术情报研究所 A method of extracting asiatic acid from centella
CN109320579A (en) * 2018-10-30 2019-02-12 天峨县科学技术情报研究所 The extracting method of Gotu Kola P.E
CN114014904A (en) * 2021-11-19 2022-02-08 湘南学院 Method for rapidly preparing high-content asiaticoside from asiatic pennywort herb raw material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1244036A (en) * 1998-07-31 2000-02-09 西门子公司 Device and method for forming controllable isolating layer on top of deep channel
CN101200487A (en) * 2007-11-27 2008-06-18 浙江大学 Method for preparing asiatic centella total saponins by using macroporous adsorption resin
CN102603854A (en) * 2011-01-25 2012-07-25 苏州宝泽堂医药科技有限公司 Method for extracting asiaticoside from asiatic pennywort herb

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1244036A (en) * 1998-07-31 2000-02-09 西门子公司 Device and method for forming controllable isolating layer on top of deep channel
CN101200487A (en) * 2007-11-27 2008-06-18 浙江大学 Method for preparing asiatic centella total saponins by using macroporous adsorption resin
CN102603854A (en) * 2011-01-25 2012-07-25 苏州宝泽堂医药科技有限公司 Method for extracting asiaticoside from asiatic pennywort herb

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109320580A (en) * 2018-10-30 2019-02-12 天峨县科学技术情报研究所 A method of extracting asiatic acid from centella
CN109320579A (en) * 2018-10-30 2019-02-12 天峨县科学技术情报研究所 The extracting method of Gotu Kola P.E
CN114014904A (en) * 2021-11-19 2022-02-08 湘南学院 Method for rapidly preparing high-content asiaticoside from asiatic pennywort herb raw material

Also Published As

Publication number Publication date
CN106366152B (en) 2018-01-19

Similar Documents

Publication Publication Date Title
CN106349320B (en) The method that asiatic acid is extracted from centella
CN106366152B (en) The method that asiaticosid is extracted from centella
CN104610410A (en) Extraction process of ginseng saponin Rd
CN106380504B (en) The method that madecassoside is extracted from centella
CN103739586A (en) Method for extracting diterpenoid compounds from Blumea aromatic DC.
CN1869055A (en) Method of extracting and separating ginseng saponine monomer from ginseng leaf
CN106176848A (en) The method extracting asiatic centella total saponins from Herba Centellae
CN101698059A (en) Method for separating dendrobium total alkaloids by ion exchange resin
CN106336448B (en) The method that brahmic acid is extracted from centella
CN102172361A (en) Method for separating traditional Chinese medicine total alkaloids by ion exchange resin
CN106214710A (en) The method extracting triterpene acid from Herba Centellae
CN106420871A (en) Preparation method of Panax notoginseng saponins rich in Fe and Fd and monomers Fe and Fd thereof
CN100582119C (en) Process for separating diol ginsenoside and triol ginsenoside
CN107903296A (en) The extracting method of madecassoside
CN101697983A (en) Method for separating pegamun harmala total alkaloids by ion exchange resin
CN101698057A (en) Method for separating anoectochilus formosanus total alkaloids by ion exchange resin
CN1869056A (en) Method of extracting and separating ginseng saponine mixture from ginseng leaf
CN101491631A (en) Method for separating verticine total alkaloids in traditional Chinese medicine extract
CN110845553A (en) Method for extracting gastrodin by ultrasonic water bath heating
CN107936081A (en) The extracting method of asiaticosid
CN107739399A (en) The extracting method of brahmic acid
CN101697982B (en) Method for separating common camptotheca fruit total alkaloids by ion exchange resin
CN101698003B (en) Method for separating rhizoma corydalis total alkaloids by ion exchange resin
CN101697986B (en) Method for separating catharanthus roseus total alkaloids by ion exchange resin
CN103690587A (en) Preparation method of triterpenoid saponin component

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180108

Address after: 530100 the Guangxi Zhuang Autonomous Region Wuming District of Nanning City Yilin Development Zone

Patentee after: GUANGXI MAIKE JIANFENG PHARMACEUTICAL Co.,Ltd.

Address before: Room B303 block B District No. five building, 541004 the Guangxi Zhuang Autonomous Region seven business district of Guilin City air Mingxi Road New District

Patentee before: GUILIN BATURAL INGREDIENTS Corp.

TR01 Transfer of patent right

Effective date of registration: 20220701

Address after: 541000 room 415, 1, University Science Park, Guilin National High tech Zone, No. 108 Qilidian Road, Qixing District, Guilin, Guangxi Zhuang Autonomous Region

Patentee after: Guilin taikrypton Biotechnology Co.,Ltd.

Address before: 530100 Yiling Development Zone, Wuming District, Nanning City, Guangxi Zhuang Autonomous Region

Patentee before: GUANGXI MAIKE JIANFENG PHARMACEUTICAL Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220902

Address after: 530100 No. 22, District D, dingluo District, biaoying community, Wuming District, Nanning City, Guangxi Zhuang Autonomous Region

Patentee after: Nanning Chengtai Biotechnology Co.,Ltd.

Address before: 541000 room 415, 1, University Science Park, Guilin National High tech Zone, No. 108 Qilidian Road, Qixing District, Guilin, Guangxi Zhuang Autonomous Region

Patentee before: Guilin taikrypton Biotechnology Co.,Ltd.

TR01 Transfer of patent right
CP02 Change in the address of a patent holder

Address after: No. B-2, Yiling Industrial Concentration Zone, Wuming District, Nanning City, Guangxi Zhuang Autonomous Region, 530100

Patentee after: Nanning Chengtai Biotechnology Co.,Ltd.

Address before: 530100 No. 22, District D, dingluo District, biaoying community, Wuming District, Nanning City, Guangxi Zhuang Autonomous Region

Patentee before: Nanning Chengtai Biotechnology Co.,Ltd.

CP02 Change in the address of a patent holder